US2008200721A1PendingUtilityA1

Mdi Production By Means of Liquid Phase and Gas Phase Phosgenation

Assignee: BASF AGPriority: Mar 30, 2005Filed: Mar 22, 2006Published: Aug 21, 2008
Est. expiryMar 30, 2025(expired)· nominal 20-yr term from priority
C07C 263/10C07C 265/14
43
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Claims

Abstract

The invention relates to a process for preparing isocyanates, which comprises the ( 1 ) preparation of a crude MDA mixture by reaction of aniline with formaldehyde, ( 2 ) separation of the crude MDA mixture into MMDA and PMDA, ( 3 a) phosgenation of the PMDA separated off in step 2 in the liquid phase to form PMDI and ( 3 b) phosgenation of the MMDA separated off in step 2 in the gas phase to form MMDI.

Claims

exact text as granted — not AI-modified
1 - 4 . (canceled) 
     
     
         5 . A process for preparing isocyanates, wherein said process comprises:
 (1) preparing a crude MDA mixture by reacting aniline with formaldehyde;   (2) separating said crude MDA mixture into a gas phase comprising MMDA and a liquid phase comprising PMDA;   (3a) phosgenating said PMDA in said liquid phase separated off in (2) to form PMDI; and   (3b) phosgenating said MMDA in said gas phase separated off in (2) to form MMDI.   
     
     
         6 . The process for preparing isocyanates according to  claim 5 , wherein said reacting of aniline with formaldehyde in (1) is carried out at a ratio of aniline to formaldehyde ranging from 2 to 5.5. 
     
     
         7 . The process for preparing isocyanates according to  claim 5 , wherein said separating of said crude MDA mixture in (2) is carried out so that said MMDA separated off comprises a maximum content of PMDA of 12 wt. %. 
     
     
         8 . The process for preparing isocyanates according to  claim 5 , wherein said separating of said crude MDA mixture in (2) is carried out so that said PMDA separated off comprises a maximum content of MMDA of 30 wt. %.

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